Process and apparatus for the electrical treatment of liquids and fluids, and the products resulting therefrom.



v 1. BLOOJML V PROCESS AND APPARATUS FOR THE ELECTEHCAL IREAIMENT OF- LIQUHJSv AND FUUIUS, AND THE PRODUCTS RESULTING IHEREFROM.

A'PPLLCATIONQ FJLED MAIL 3.1,, 8L5.

process of treating JACOB E. BLOOM, OF BROOEJYN, NEW iiOB-K.

PROCESS Specification of Letters Patent.

ANDAPPABATUS FOR THE ELECTRICAL TREATMENT LIQUIDS AND- FLUIDS, AND THE PRODUCTS RESULTING THEBEFROM.

Application filed March 31, 1915. Serial 1T0. 18,325.

electrical and adsorption means,kof hquids,

0r fluids, and particularly aqueous or alcoholic or combined aqueous and alcoholic liquids, suchas beer, malt extracts, and the like, and with the object of removing there- ,from certain adsorbable colloidal impurities or constituents such as turbidity or sedi- 2o 'ment-forming, colloids, which are not removed by ordinary filtration, and to" give to the resulting liquids-new and valuable properties: V

This application is in part a continuation with improvements of U. S. Patent, Serial No. 84232 1st, 1914.

This invention comprises certain novel forms and constructions of apparatus, as Well asrnovel methods or processes of treatment, and the'novel products resulting from such treatment.

As a process,

filed June my invention comprises a liquids or fluids, such as those referred to herein by subjecting the same to the influence of an alternating electric field or a magnetic field, or an alternating field from A. C. source, or a combination thereof, under control as to voltage and frequency and amperage, in the presence of a mass of a suitable comminuted solid, insoluble electrically-acting adsorption material, advantageously and preferably a dielectric, the liquid or fluid being1 passed intermit tently or continuously t rough the inter stices of said adsorption material in the electric field, under regulated temperature and pressure; and. being advantageously in a chamber of a suitable container-such as sorbed ions,

my ap lication forstituents,

maintained during and after treatment in an insulating or non-conducting vessel, or

receptacle, together with means for supplyng and removing from said chamber, either intermittently or continuously, a liquid or fluid, to be treated, and means for controlhng the rapidity of such passage when continuous; and means maintaining in said mass and chamber and the liquid or, fluid therein oropassing therethrough, a suitable alternating electric field such as a magnetic or electromagnetic field, a' magneto-electric field, and electrostatic field and the like, with. means of control thereof; and with regulable means of at 'temperating the said chamber and liquids and material to any desired temperature.

from such treatment, said product containwith an enhanced electric charge or ad- 'sorbable or not permanently adsorbable (being first adsorbed and then electrostatically repulsed) by ing electric field, and said product being substantially free from, or containing to a materially decreased extent, colloidal constituents, particularly suspensoids, adsorbable by such adsorption material, under such influence; said product in some cases, as in the case of beer or fermented beverages containing the valuable assimilable emulsoids on non-adsorbable or amphoteric colloidal constituents, in stable equilibrium due to such charges, or state of electrification, but being relatively or substantially free from the adsorbable or suspended colloidal consuch as are the turbidity and sedinhilcnt-forming colloids of beer, ale, and the e. i The invention as thus brieflyoutlined will be hereinafter more fully set forth. In the ordinary purification processes applied to beverages, such as beer, ale, etc., or

particles of colloidal nature, in colloidal solution or state, is difiicult to effect. Moreover some colloidal constituents, especially Patented Nov. 30, 191 5.

the comminuted adsorption "material under the influence of the alternatfor producing and i As a product, my invention comprises the 7 novel stabilized liquid or fluid resulting colloidal constituents (particularly slmdry emulsoids) which are non-ademulsoids, are often valuable and should be retained in Solution, while others should be removed. Ordinary filtration processes are in some cases effective in removing certain colloids, but in general all colloids including those which it discriminately removed. Chemical precipitation processes have been proposed for the purpose of coagulating and throwing out of solution and thus removing such colloids, ,but such processes also tend to remove all colloids, including the valuable more perma'-' nent emulsoid colloids, and moreover such chemicals may contaminate the liquids, and dilute them. In the case of certain liquids and fluids it frequently the most careful purification and filtration processes, there occur subsequent separation of colloids causing turbidity or sediment, particularly in the case of beverages and extracts such'as beer, and contains appreciable amounts of colloidal constituents of. an emulsoid nature after the fermentation. It is desirable that these emulsoid colloids which in may cases have valuable nutritive or tonic properties should be retained and kept from precipitation, while the undesirable colloids of a suspensoid nature should be removed.

lhe present invention relates to the treatment of such liquids or fluids in order to efiect the selective purification referred to, where constituents capable of being separated in this way are present.

It further relates to the treatment of liquids and fluids, generally containing colloidal constituents together with non-adsorbable or amphoteric constituents, in order to remove and separate or adsorb such adsorbable constituents.

l have found that, if a liquid or fluid containing adsorbable colloidal constituents is subjected to the influence of an alternating electric field in the presence of a suitable comminuted adsorption material, it is possible to adsorb upon such material, adsorbable colloidal constituents and to otherwise promote the flocculation or precipitation or coagulation or aggregation of suspensoids and turbidity-causing particles, including such as metallic or inorganic and organic colloids,

or iron or other colloidal solutions of copper amorphous mat er, albumetal hydroxids, mens and proteins coagulating spontaneously, certain nucleo-proteins, globulins,

gluten-turbidity causing particles, the complex proteins and substances ordinarily found in cooler sludge or deposited in trade casks and bottles, etc.,+while never-. theless retaining in solution in the liquid or uid certain valuable colloidal constituents of an emulsoid or amphoteric nature, the process thus effecting a selective purification in a particuhrly advantageous manner. I use the term alternating electric field to refer to and include various fields obtainis desirable to retain are inhappens that aftermeans able from alternating current source, preferably symmetrical, or of an alternating nature obtained from other current source, such as the field induced by an electromagnet or an electromagnetic coil, or by a magneto-electric coil, or by electrostatlcally charged electrodes or by an electrostatic field or other induced field; orby'an alternating'current between electrodes or terminals immersed in the liquids or fluids; and the like. I Y I For aqueous liquids, and other liquids of a similar nature, alternations .of low frequency are usually more advantageous in induced fields. Fo'r heavy; oils such as cotton-seed, etc., and blends of oils and fats, and more viscous solutions such as glycerin or sugar syrup, a current of very much higher frequency and voltage is more advantageous. It will be understood that the nature of the current and its voltage can be varied within rather wide limits, so long'as the alternating field of suitable character is obtained.- p h With beer and most liquids I prefer-a medium frequency and.low density of current and symmetrical currents for the systern of apparatus herein illustrated, z. e.. where alternating current is 'passedbetween, electrodes immersed in' theivessel and liquid; with such the current frequency and current density should be such as to avoid any substantial electrolysis at the electrodes. If the frequency and density do not avoid such electrolysis then the frequency or density or 'both should be increased or decreased until there is no electrolysis. on the other hand where the induced electric fields are used as illustrated in the apparatus in my afor esaid prior application I advantageously use .the low frequency of 16 or 25 or 60 cycles. By medium frequencies I mean from 100 to about 1,500 cycles. By high frequency I mean such as is used with wireless telegraphy.

For my electrodes herein, which must be of insoluble materials, I advantageously use platinum or carbon for acid and neutral solutions, liquids and fluids, and iron for alkaline.

As adso tion materials, there can be used many Seli insoluble and inert materials, advantageously dielectric but electricallyacting when immersed in the liquid or fluid,-

and having a conductivity less than that of the liquid or fluid. The adsorption material should be relatively speaking a non-conductor but itself advantageously capable of being charged or have electrostatic capacity and should advantageously be com lementary to the colloids or particles which it is desired to adsorb. That is to say,.where in solution, the'adsorbable or suspen oid colloids are normally electronegative, they are might be detrimental in foods, oils, beverages, pharmaceutical preparations, and the like. Again, insolutlons where the colloid or particle would be disengaged at or would migrate toward the cathode, in an electrolytic cell, with a direct current, there it is electropositive; and there I use my process with an electronegative adsorption material to attain colloid precipitation, without addition of extraneous chemicals. I prefer to use as an electropositive adsorption material in conjunction with the alternating electric field, a large mass of comminuted solid corundum or crushed abrasive garnet z'. e.,

of 16 to 30 mesh; and I prefer comm1nute solid pure quartz of about the same mesh as an electronegative adsorption material. I apply the term suitable adsorption material as indicative of its said property, '5. 6., being electropositive to adsorb negative colloids; and vice versa. The adsorption material should be in a suitable state of comminution, advantageously coarse, e. g.- 16 to 30 mesh, and should advantageously be of a crystalline nature. Among the materials which may be included as adsorption materials, may be mentioned pure quartz, and particularly the purer forms of silica sand; some forms of glass; abrasive garnet corundum; crystalline carborundum; zeolite; kam lin, preferably of scale like crystalline form; emery; asbestos, etc. Also crushedogranulated glass; stoneware; porcelain; V and mica; also sundry mineral fibers such as asbestos thread, woven asbestos fabric, glass .wool, etc. Also fullers earthytalc; infusorial silica; kieselguhr; sundry typ 'tripoli, meaning the light porous silicious es of rock, crushed, from which the calcareous material has been leached; pumice or lava having a loose spongy or cellular structure; rottenstone, a crushed silicious limestone from which the calcareous part has been wholly removed, etc.

When the liquid containing the adsorbable colloids is subjected to the influence of the alternating electric field in the presence of the adsorption material, this material .being itself charged by immersion, will attract colloidal particles carrying an opposite electric charge, and repel those carrying the same electric charge. Colloidal particles of an amphoteric nature, such as the emulsoid colloids, are capable of changing their charge so that .if first attracted to the adsorption material, they will upon contact have their charges neutralized and be then charged oppositely and repelled; or de-adsorbed; while suspensoid colloids, which are not amphoteric and generally negative will be in general attracted to the adsorption material and upon contact will have their charges neutrallzed and willremain or be adsorbed by or upon the adsorption material. The alternating nature of. the field causes a rapid to and fro movement of the colloid particles and the charging of the latter from adjoining ions and favorably influences the adsorption process.

As a result of this process, the liquid or fluid treated is freed from a greater or less amount of its adsorbable colloidal constituents, while the non-adsorbable constituents such as the amphoteric colloids and colloids not adsorbable under the.- particular condi-.

tions of the treatment remain in the liquid. Where the liquid contains adsorbable colloids in part normally electro-negative and in part electro-positive, or amphoteric, it is advantageous to subject the material first to the adsorption action of a material normally electro-positive and then to the action of a material normally electro-negative; whereby a larger proportion of the colloids are adsorbed, etc.

Where the liquid treated contains non-adsorbable colloids such as the amphoteric or emulsoid colloids,the treated liquid will have been not only freed by the above process from part or all of its suspensoid or adsorbable and non-reversible colloids, but it still retains in a particularly advantageous condition, said repulsed or non-adsorbed or. deadsorbed amphoteric particles, since these colloids as the result of the treatment have adsorbed ions or have been given an electric colloids of a particular nature with enhanced charge.

In the case of liquids containing spontaneously coagulable colloids such as some of the albumens, the treatment of the present invention results in the coagulation and precipitation or aggregation or flocculation or adsorption of such colloids, and hence their removal as aforesaid; while the more permanent emulsoid colloids will be relatively less affected. It will be understood that colloids and other particles may also be concentrated, aggregated, flocculated, coagulated.or precipitated in the liquid or fluid by the influence of the electric field and that such substances may be also thus removed by i the adsorption material, acting like more ,erihanced charges upon other particles conmaterial with its charges due to immersion: In order to retain upon the emulsoid col loids and other amphoteric particles in solu tion the electric charge to keepthe same in;

, stable solution, I advantageously use an in art electrode, preferably a platinum ,plate,, within the interior of the vessel leading'tol; the adsorption material, in contact with the therein or with the.v

pipe or conduit en route thereto, or

' said particles,

tinuing in solution due to the meeting of influenced by said alternating field, at the interface of the solid adsorption passing liquid or fluid liquid in therefrom, or wherever it is a continuationof the fluid in the adsorption vessel, and distant from or beyond the influence of the electric field; and which plate is in electrical connection with an insulated ground wire having an insulated exterior interrupter which automatically breaks the earth connection with each'cycle of the alternating current used in the process,-and preferably breaking connection with the negative alternation where the adsorption material is electropositive,and with such positive alternation where said material-is electronegative.

In'some cases of liquids arid fluids,-generally other than Vbeverages,it is an object the liquid not the emulsoids,

ac. practically all colloids, both amphoteric and other-wise;-'this I accomplish, by using my same apparatus and process with supplemental treatment by mechanically-acting solid insoluble adsorp- .tion material,advantageous1y under noninsulated conditions; such material being most advantageously a pure cellulose, preferably a mass of cotton fiber or numerous surfaces of cotton cloth,or amass of charcoal preferably animal charcoaL' The pre- 'cipitates, coagulations, flocculations, aggregates, adsorptions and the like, found on such cellulose after such passage as well as those found on the prior adsorption material, can be readily gathered as concentrates together or separately, and in the mann r now practised in chemical laboratories in gathering such from ordinary fi ltrations; e. g. by burning the cellulose.

The process of the present invention,

which is more particularly described in its application to beer and other products from malt, such as malt extract, is also of general application for liquids and fluids, such as: beveragesincluding cider, whisky, spirits, brandy, cordials; vinegar; an milk and liquid milk products; mineral waters;

able, but are notelectrolytes;

passage through a meagre pharmaceutical liquid preparations, decoc tions, extracts; liquid coffee and tea; bacteriological preparations, especially serums and vaccins; water purification; syrups, honey, molasses; aqueous and alcoholic manufactures, liquid blends and extracts; organic compounds such as turpentine oil; ferments; yeast; colloidal solutions of dyes and 1 dyestufi compounds; hydrogenated products where catalysts have been used; oils, fats and fatty acids and blends and waxes in liquid state; mineral solutions of liquids and fluids from ores and generally in the refining of sugar juices, such as cane {or beet juices, etc., and in the'concentration of liquids; in condensation of fluids; also of glazes and the like in ceramics; and in salting' out of liquids but without salt; in purifying liquids; also of emulsions to aggregate and obtain the colloids therefrom; and other liquids and solid substances capa ble of innocuous conversion to liquid state and vice versa, and containing colloidal constituents adsorbable under the influence of 1 lactic fermentation thereof. Beer and the I like capable of this treatment comprise mostly water, with dilute solutions of electrolytes and of non-electrolytes, including emulsoid colloids which are non-adsorbable I (permanently) and colloids which are adsorband including albuminoids, proteins, organic acidsor alkali or salt solut ons, mineral substances, mucilaginous substances, pectins, and electroindiflerent substances such as sugar and alcohol. Beer and the like also contains fermented and unfermented extractive matters;

protozoa; bacteria, yeast, etc.; and amor- -phous matters from the vessels and conduits used in the manufactures. 1 1

In the art of brewing I interpolate my electric adsorption treatment as an additional. process, advantageously at the three following present manufacturing stages 1) and (2) and (3") below, or after the latter twoonly prior to packaging in trade barrels,' casks,

or bottles, tow1t:

(1) :-Before mixing and boiling the mash copper kettles,

or wort with, hops in the or after the fermentation only, and

i. e.- when the mash has been completed and.

when there is resent therein an excess of active dlastase whose actlvlty in further converting. starch into sugar it 1s desired to stop), there, in lieu of using what is known 7 as the'underback, I substitute my said process advantageously at temperature of about 130 degrees F., to remove said diastase and otherwise remove amorphous substances from the mash (2): After, the boiling of the hopped wort, I use my process\advantageously at about degrees F. A well boiled hopped this evil.

wort, 2'. e. before the fermentation, which finely divided amorphous matter. is fer-- mented with yeast,little or no change is produced in the suspended matter, either in appearance or its state of aggregation and the fermented liquid shows the same resistance to filtration and centrifuging as did the original wort. Such turbidity-causing substances, also have a distinct toxic action on the yeast.

' (3): And again-and preferably, after the fermentation step. Sundry complex proteins are ordinarily found depositedfrom beer in the storage vats and kegs, showing that mere filtering, as heretofore commonly practised, does not avoid or remove the cause of gluten-turbidity, etc. My process following the fermentation largely avoids I pass the liquids through the adsorption materials, advantageously first electropositive (such as corundum) and then electronegative (such as quartz) held in a suitable dielectric or insulated vessel or tube, and subjecting it therein during such passage to the alternating electric field. In cases such as beer and malt products where it is desired to retain emulsoid colloids in stable solution, the adsorption material I finally use is advantageously electronegative, in order to confer negative charges on such colloids to most advantageously protect the same against precipitation as'long as the liquid is efliciently insulated. Conversely, there are sundry liquids, especially pharmaceutical, wherein it is desirable, for sundry reasons, to confer positive ions or charges upon its amphoteric colloids, and, in such cases, the final adsorption material to be used with my process, is advantageously, electropositive, such as crushed abrasive garnet or corundum. Beers, liquid extracts, and the like made from the same species vary in their constitution, just as grapes grown in the same fields vary from year to year, and the specific treatment can readily be varied in accordance with the variations in the liquid to .betreated.

After the liquid has been treated as herein described, and thereafter kept in insulated conditions,any of the ordinary tests as to taste or quality or appearance or bouquet or turbidity or stability or chemical decomposi- Lion after placing in glass or other dielectric container, should disclose an unsatisfactory condition or state as regards such or other advantages herein described, then the process may be repeated andthe rate or speed of passage of the liquid, through the electric field and adsorber, or alternating currents of more or less voltage or frequency or amperage, or a greater or lesser magnetic or other alternating electric field, or more or less adsorption material, or different kind of latter may be used, to overcome such objections.

In my application Serial No. 842327, filed June 1st, 1914, I have illustrated and described and claimed certain other types of apparatus; in which the novel process of the present invention can be practised. Such apparatus is generally similar to tha't of the present application, in that it comprises a body of a suitable comminuted solid adsorption material in an insulated container and receptacle for liquids or fluids, together with means for providing and maintaining in said receptacle or container, and the liquid therein, or passing therethrough, a suitable alternating electric field; but it is distinguished from the apparatus of the.- present application in that the field is induced, while the field of the present invention is a field between electrodes, such as is obtainable, for examplebetween electrodes in a non-electrolytic cell. In my said prior application Serial No. 842327, I have also described and claimed the process of treating liquids by the combined influence of a body of comininuted solid adsorption material and an alternating electric field, the electric field however being limited in the amended specification to'an induced field as distinguished from the field between electrodes, utilized in the embodiments of the invention specifically described and claimed in the present application; while in the present application, I

claim such process generically for liquids suchas beers, which present peculiar difii-' culties in their purification, because of gluten-turbidity tendencies, etc., and which are by my process converted into a novel,

valuable product substantially freed from such turbidity-forming adsorbable colloids,- such as suspensoids, while still containing the valuable non-adsorbable emulsiod 001 loids in stabilized conditionfiwhich have 7 electrically adsorbed ions from the immersed I adsorption material due to my process; such retained colloids having valuable nutrit ve or tonic properties.

In general, the apparatnsand-processfof my said prior application en body-pqniva lent or corresponding elementgputj ngi dip.

ferent types of apparatus have their own particular advantages, due to the difi'erent alternating electric fields utilized and to the different arrangements of electrodes, etc.

In order to illustrate the invention more fully I have illustrated on the accompanying drawings certain forms or constructions of apparatus embodying the invention and in which the process of the invention can be practised; but it is intended and understood thatthe invention .is illustrated by, but it is not limited to the embodiments thereof so illustrated and described.

certain embodiments of the invention, Figs.

1 and 2 illustrate two forms of apparatus suitable for use together or separately. The

apparatus of Fig. 1 is made up of a contamer or vessel A with dielectric lining A, said vessel being advantageously of glass or other suitable insulator or dielectric material.- The vessel is shown as having an intermediate inwardly projecting ledge, supporting a perforated plate upon which is placed a layer 8 of relatively coarse material and then the main body sof the com minuted adsorption material of the nature in}; provided with a alreadydescribed. A perforated plate 7 at the top of the apparatus Fig. 1 serves as a distributing plate and for removing coarse particles from the incoming liquid or fluid. Below the body of adsorption material is a compartment for receiving the liquid or fluid from such body, this compartment bemanhole P for cleanmg purposes, etc.,- with a tubular coil w for introducing reverse stream of water or water and steam for cleaning ;,with a valve controlled outlet 6 for drawingofi' the liquid, and with a second valve controlled outlet 3 leading to the inlet 6 of the apparatus of Fig. 2. The outlets b and e are protected by a screen 0 of suitable construction for gathering sediment or fiocculated I or precipitated or suspended particles, eta, "and preventmg their escape;

body S of adsorptionmaterial'are. arranged two series of electrodes. El and-E with each other and each series being con,- nected by suitable 'con'necti ns-t bus ba-rs G and Gr" connected with asuit'able "alter- 1 withi he:

alternatin nating current-source as shown. An -auxil-' iary electrode-like plate H over which the means (not shown).

ings at the top, theinner casing T liquid passes is also arranged within the vessel of Fig. 1, above o'rbelow, or in the electric H The apparatus of Fig. 2 is arranged to receive the liquid from the vessel Fig. 1, and to give such liquid a further treatment where such treatment is desired. This apparatus is made up of a container or receptacle D with dielectric lining D having a removable cover and divided by the filtering or adsorption layer 8 arranged between per- --forated plates N, into two compartments-y and y, the electrodes E and E being arranged on opposite sidesof said layer. The apparatus is provided with. inlet connection 6, outlet u and valve controlled outlet pipe V leading to a suction or vacuum providing shown.

In the apparatus of Figs. 4 and 5, the receptacle or container is made up of outer and inner casings T and T, with dielectric linings A and A between which the body of adsorption materialiis placed. A'cover, which may be removable, connects these casis supported also at the bottom by posts Jfrom theiouter casing. The body S-of adsorption material is shown as supported much the same as in Fig. 1, and from the bottom of the apparatus outlets band a are provided with suction connection V much the same as in Fig. 1. The lower part of the apparatus of Fig. 4, is however divided into two compartments 3 and y corresponding to the compartments ofthe apparatus of A water gage m'is also Fig. 2, and a. filter cloth 0 on adsorption layer 8' is provided but without any electrodes being shown. A second suction out-' let connection is shown at V. Surrounding the apparatus is a heating or cooling coil 0' and a central coil cf'" is also provided, either or both of which may be used as desired. The electrodes E, E and E of Figs. 4 and 5 are arranged concentrically and op-' positely'as clearly illustrated, three sets of electrodes being shown for three phase cur.- rent. The apparatus of Fig. 4 can also be connected with and operated with theappara'tus of Fig. 2 js'imilarly as may that of In the carrying out of the process of the present invention, in the apparatus described, the liquid or fluid to-betreated is introduced through the perforated distributing plate 7 of Flg. L-or the inlet 6? of Fig.

4, and enters-the body of adsorption material and the almrnating electric field. The treatment may be intermittent, the liquid alternately introduced and discharged,

preferable for myelectric adsorption of colloids and 176 degrees F. for incidental sterilization purposes. During the passage of the liquid through the adsorption material, it is subjected to the alternating electric field between electrodes in order to attain the above described eifects. After such passage and treatment, the liquid can be drawn 0 at b, or passed through the second layer of adsorption material Fig. 2 and then drawn oif at u. If the body of adsorption material 8 is electropositive, the body .9 is advantageously electronegative, or vice versa, in order that the liquid may be subjected to such materials and opposite and complementary forces, successively, and a double adsorption effected accordingly. The adsorption material a may be of comminuted corundum (generally electropositive') or comniinuted quartz (generally electronegative) orxm'aterial such as has alread been described. The material 8 may a vantageously be of asbestos or similar material and may in some cases serve merely as a filter and in others as an adsorption body under the influence of the electric field. Or 8' may be enlarged to a mass of comminuted adsorption material of opposite sign to s, in a readily understood vessel, not shown.

When any considerable accumulation of sediment, precipitations, fiocculations, ad-

sorptions, or solids has occurred in the lower body a, the cover of the apparatus'of Fig. 2 can be removed for cleaning purposes; or in the apparatus of Fig. 4 the fastener R canbe loosened, and the lower part of the apparatus swung around on the pivot R, and access obtained to asbestos or cotton cloths O and 0' supported by dielectric perforated sieves and from which sediments and the like can be gathered by well known facilities, when such are to be saved. The outlet P of F' 1 similarly enables cleaning of the screen When the adsorption bodies or layers have become clogged or saturated, it may in some cases be necesasry to renew such bodies. In other cases the separated colloids can be dissolved by suitable solvents (acids, bases, etc.,) and removed. Where 55 the adsorption materials have become satuor the process may be continuous by proprated with adsorbed colloids which it is de-' sired to obtain and separate, such materials may be suitably treated with solvents 0 otherwise to obtain such colloids.

The alternating current may be of any suitable frequency and amperage, advantageously of low frequency 16 to 25, and

.especiallywith induced alternating fields produced from any suitable source, either alternating current, of by suitable pole changers from direct current. It will be understood that high frequencies and voltages especially with A C field in the electrolyte cell type betweenclectrodes may be more advantageous in some cases as with oils and low medium frequencies advantageously in others as with beer. It will also be understood that poly-phase currents ofvarious kinds can be used, Fig. 5 showing electrodes duced fields such as described and claimed in my above prior application. That is to say, the electrodes are arranged alternately or oppositely and create a narrow field between them to which the liquid being treated is subjected while passing over the adsorber loosely packed between the electrodes. Va

rious arrangements of such electrodes can 105 be effected, and in parallel or in series, as

will be readily understood. The electrodes may be of any suitable material, preferably platinum or platinum-iridium or aluminum, or other metal advantageously covered with dielectric material such as glass, etc., which will not injuriously aifect or be aflected by the liquid, undergoing treatment. The apparatus of the present invention has the advantage that it is capable of wide application, and that the size can be varied within wide limits, aswill be understood. By increasing the size of the electrodes or their number and by correspondingly increasing the size of the apparatus it is possible to use a large body of the adsorption material therebetween and to treat a correspondingly large body of liquid, while still maintaining the electrodes relatively close together and keeping the. liquid and the adsorption material in thin layers therebetween. The receptacle and its connections should advantageously be insulated or advantageously made of glass or other insulating or dielectric material and the container into which the treated liquid is discharged should also advantageously be of such material,in other words during and after said passage of the the adsorption material, I do not restrict myself to thus OPerating While in the state of passage through the vessels, but may also attain the result. sought, but with less quantity, by analogous treatment and means whereby the liquid is agitated in a dielectric vessel, in contact with solid comminuted adsorption material, in an alternating electrio field,-and the ensuing periodical withdrawal therefrom and renewal thereof.

The liquid after treatment carries electric charges from the alternating current source and further enhanced by adsorption of ions by the emulsoids from the adsorption material,the opposite charges due to polarization having been removed by the ground connection.

The adsorbed colloids or sediment-forming constituents may be retained by the adsorption material or they may be precipitated, aggregated, flocculated, agglomerated, or coagulated and thrown down in such form that they canbe subsequently removed by settling or'filtering or otherwise. The filter layer 0 over 8 of Fig. 4: or the adsorption layer s of Fig. 2 may effect such separation. After treatment the escaping liquid is advantageously placed in insulated containers such as bottles, etc., so that it will retain its electrified state. The liquid may in some cases be concentrated to a syrupy or even a solid consistency, or again the" liquid may be of such nature that it will remain fluid, while hot but solidify on cooling, the adsorption treatment in the latter case being ef fected while the material is heated tofiuidity. The material whether liquid orisolid is generally characterized by containing the unadsorb'able colloids such as the amphoteric colloids, and the emulsoids, which are not' permanently adsorbed and permanently retained, being first attracted and then repulsed by the' adsorption material; arid by its freedom or substantial freedom from adsorbable colloids such as the suspensoid colloids which are non-amphoteric. Accord inglyinthe case of Liquids treatedv by my" process, such as beer or wine or other aqueous oralcoholic beverages or extracts the liquid, for example beer, may be substantially free from}. the objectionable turbidity-forming suspensoid colloids, while still containing the valuable emulsoid. colloids; and particularly when freshly treated, the products will in general contain the colloidal constituents, the emulsoids with enhanced electric charges, and adsorbed ions and accordingly in an electrically stabilized condition; the said emulsoids carrying adsorbed ions obtained liquid or fluid to 1,1ca21a by physical, electric and adsorption means and not by chemical means. such as result in new complex chemical compounds. 1

It will be understood that wherela single treatment is not suflicient,,.the' treatment can be repeated one or more times with the same or different ads'orptioltmaterials and with different strengths and frequencies ofcurrent. The subsequent treatments may advantageously be through adsorption materials complementary to those first utilized in order to obtain the double adsorption action.

While I have illustrated and described certain specific forms of apparatus and have and temperature through a mass of comminuted, solid, suitable adsorption material which is electronegative in liquids and fluids of an acidic nature, and electropositive in liquids and fluids of a basic or of a neutral nature, and simultaneously subjecting the the action of an alternating electric field of regulated voltage, frequency and amperage, under insulated conditions, the same having a make and break electric connection to earth in synchronism with said current; and thereafter maintaining the liq- 1 uids and fluids under insulated conditions.

2. In the treatment of liquids and fluids,

the process which consists in passing the liquids orfluids, under regulated pressure and temperature through a mass of comminuted, solid, suitable adsorption material,

which is electronega'tive in liquids and fluids of an acidic nature, and electropositive in liquids and fluids of a basic or of a neutral nature, and simultaneously subjecting the liquid or fluid to the action of electric field of regulated voltage, frequency and amperage.

3. In the treatment of liquids and fluids, the process which consists in passing the liquids or fluids, under'regulated pressure and temperature through a mass of comminuted, solid, suitable adsorption material,

which is electronegative in liquids and fluids of an acidic nature, and electropositivein liquids and fluids of a basic or of a neutral nature, and simultaneously subjecting the liquid or fluid to the action of an alternating electric field between, electrode terminals from an. alternating current source, of regulated voltage, frequency and amperage.

4. The process of treating liquids and fluids containing adsorbable. colloidal conan alternating tric field in the ternating electric field.

stituents, which comprises, subjecting the same to the influence of an alternating elec- I presence of a comminuted solid insoluble adsorption material.

5. The process of treating liquids and fluids containing adsorbable colloidal constituents, which comprises passing the same through a mass of solid insoluble comminuted adsorption material, and subjecting the same during such passage to the influence of an alternating electric field.

6. The process of treating liquids and fluids "containing adsorbable colloidal constituents, which comprises passing the same througha mass of comminuted solid insolumaterial in a non-conducting such passage to the influence of an alternating electric field.

7 In the treatment of liquids-and fluids, the process which comprises passing the same through a mass of comminuted, solid, suitable, electrically-complementary adsorption material and subjecting the same during such passage to the influence of an alof liquids and fluids, the process which comprises passing the same through a mass of comminuted, solid, insoluble, suitable, adsorption material which is electrically-complementary to same and subjecting same during'such passage to the influence of an alternating electric field under insulated conditions.

9. In the electrical treatment of liquids and fluids, th'e'process which consists, in subjecting the same while in an electrified state from alternating current source,to the action of electrically-complementary adsorption material. V

10. In the electrical treatment of liquids and fluids, the process which consists in subjecting the same while in an electrified state from alternating current source, to the action of electrically-complementary adsorption material under insulated conditions. I

11. In the electrical treatment of liquids and fluids, the process which consists in subjecting the same to the influence of an alternating electric field while in contact with comminuted solid insoluble dielectric electrically-complementary adsorption material under insulated conditions.

12. In the electrical treatment of liquids and fluids, the process which consists in subjecting the same to the influence of an alternating electric field while in contact with comminuted solid insoluble dielectric electrically-comp'lementary adsorption material under insulated conditions.

13'. In the electrical treatment of liquids 8. In the treatment and fluids, the process which consists in subjecting the same to theinfluence of an alternating electric field while in contact with sorption material 15. In the treatment of liquids and fluids, I

the process which consists in subjecting the same to the influence-of an alternating elec tric stress from alternating current source while in engagement with comminuted solid suitable dielectric adsorption material, and thereafter'repeating the said step with adof an electric sign oppoused.

of liquids and site to that thus previously 16. In the treatment fluids, the process which consists in subjecting the same to the influence of an alternat mg electric stress between terminal electrodes from alternating current source while in engagement with comminuted solid suitable dielectric adsorption material, an thereafter repeating the said step with adsorption material of an electric sign opposite to that thus previously used, under insulated conditions.

17. In the treatment of liquids and fluids, the process which consists in subjecting same under insulated conditions, and 111 contact with comminuted solid insoluble electrically-complementary adsorption material, to 'the influence of combined multipolar electric fields from polyphase alternating current source 18. In the treatment of liquids and fluids, the process which consists in passing the liquids under regulated pressure and temperature and insulated conditions, through a mass of comminuted, solid, suitable, electrically-complementary adsorption material, and simultaneously subjecting the liquid to the action of combined fields between terminal'electrodes from polyphase alternating current source, of regulated voltage, frequency and amperage, the same having a make and break electric connection to earth in synchronism with said current; and thereafter maintaining the liquids under insulated conditions.

19. In the treatment of liquids containe ing adsorbable colloids the process which consists in subjecting the liquid to the influence of an alternating electric field while in contact with a comminuted solid insoluble adsorption material having an electrical charge, when immersed in said liquid, opposite to that of the colloids contained in said liquid.

20. In the electrical treatment of beer,

malt extract and the. like, the process which consists in subjecting the same to the 'in fluence of an alternating electric field while in contact with comminuted solid insoluble dielectric electrically complementary adsorption material under insulated condi- I tions.

trically complementary adsorption materialyand simultaneously subjecting the liq uid to the action of combined fields between terminal electrodes from polyphasealternating'current source, of regulated voltage, fre quency and,-amperage, the same having a make and breakelectric connection to earth in synchronism with said current; and thereafter repeating said step with adsorption material of opposite sign; and. thereafter maintaining and packaging the liquid under insulated conditions.

231111 the making of beers, the process' of passin'g the liquids through a mass of comminuted-solid inert dielectric adsorption material, packed loosely in an insulated vessel between sets of inert lar e plate electrodes constituting the terminals of independent alternating currents simultaneously .in operation, of a polyphase system, and

after such passage of the liquid maintaining the same in insulatedvessels and dielectric containers.

- 24. In the treatment of beer, the process which consists in subjecting the beer, before and again "after the fermentation, and after finishing the Wort thereof, to contact with acomminuted solid dielectric suitable complementary adsorption material, in an electric field from alternating current source, under insulated conditions.

25. In the treatment of beer, the process which consists in subjecting the beer, before and again after the fermentation, and after finishing the Wort thereof to contact with a comminuted solid dielectric suitable complementary adsorption material, in an electric field from alternating current source, under insulated conditions, the beer having a makea'nd-break electrical connection to earth in synchronism with said alternating current.

26. In the treatment of liquids and fluids,

acting adsorption material, under non-insulated conditions.

27 In the treatment of liquids and fluids, the process which comprises passing the same under regulated pressure and temperature through a mass of comminuted-solid in soluble electrically-actin gand complementary adsorption material, and subjecting the same during such passage to the influence of an 35 alternating electric field, of regulated voltage, frequency and amperage, under. insulated conditions, and beyond said electric field, the said liquid or fluid having a make- -a nd-break connection to earth in synchro- 9 nism with said alternations; and thereafter passing the liquid or fluid under regulated pressure and temperature through large amounts of solid insoluble mechanicallyacting adsorption material, under non-insulated conditions.

28. In the treatment of liquids and fluids, the process which comprises passing the same under regulated pressure and temperature through a mass of comminuted solid insoluble electrically-acting andcomplementary adsorption material, and subjecting the same during such passage to the influence of an alternating electric field, of regulated voltage, frequency and amperage, under insulated conditions; and thereafter passing the, liquid or fluid under regulated pressure and temperature through surfaces and large masses of loose cellulose, under non-insulated conditions.

29. In the treatment of. liquids and fluids, the process which comprises passing the same under regulated pressure and temperature through a mass of comminuted solid insoluble electrically-acting and complementary adsorption material, and subjecting the same during such passage to the influence of an alternating electric field, of regulated voltage, frequency and amperage, under insulated conditions; and thereafter passing the liquid or fluid under regulated pressure and temperature through large amounts of solid insoluble mechanically-acting adsorption material, under non-insulated conditions; and thereafter gathering from such adsorption materials, the precipitations, aggregations, flocculations, coagulations and adsorptions thereon. I

30. In the treatment of liquids and fluids containing adsorbable colloidal constituents,

. the process which comprises passing the same under regulated pressure and temperature through amass of solid insoluble electrically-acting complementary adsorption material and subjecting the same during such passagetothe influence of an alternating electric field under insulated conditions, and thereafter gathering from the adsorption material the substances adsorbed, precipitated, fiocculated,

suitable comminuted solid insoluble dielectric adsorption material, means for effect ing a flow of liquid and fluid therethrough, and means for maintaining in said chamber and mass an alternating electric field.

33. An apparatus of the nature described,

comprising an insulated chamber'holding a mass of comminuted solid, inert, suitable adsorption material in a non-conducting container provided with inlet and outlet for liquid and fluid, and means for maintaining in said chamber an alternating current field.

34. An apparatus of the nature described comprising an insulated vessel holding amass of comminuted solid, electrically-acting adsorption material; means for maintaining a combination of electric fields independently within said vessel, from polyphase alternating current source, regulated as to voltage and frequency and amperage; means for maintaining a flow of liquids or fluids through the adsorption material in the electric fieldsat regulated pressure and temperature; means for electrically connecting the said liquids or fluids to earth through an interrupter, making and breaking earth connection in synchonism with each cycle of said current; means for conveying the liquids in dielectric piping into and from said vessel into dielectric receptacles; and means for periodically cleansing said vessel and adsorption material.

35. In the electrical treatment of liquids and fluids the apparatus comprising a vessel consisting of two'concentric dielectric tubes with annular space between same holding a loosely packed mass of comminuted solid dielectric, inert, suitable adsorption material between terminal electrodes; means of passing liquids or fluids under regulated pressure and at regulated temperature through said adsorption material between electrodes under insulated conditions, and

into connecting insulated receptacles; means for maintaining within said annular space, during said passing of the liquids, and combined electric fieldsbetween said terminal electrodes from polyphase alternating current source, the terminal electrodes of one circuit facing the terminals of another circuit; means for electrically connecting the said liquid or fluid to earth through an exterior insulated interrupter making and breaking earth connection in synchronism with each cycle of said A. (3.; and means for periodically cleansing said vessel and adsorption material.

36. An apparatus of the'nature described, comprising a chamber consisting of two insulated parallel vessels having a narrow space therebetween; a mass of comminuted solid, insoluble suitable adsorption material between electrodes in said chamber; means of passing liquids or fluids under regulated pressure and at regulated temperature through said adsorption material and chamber underinsulated conditions, and into connecting insulated receptacles; means for maintaining within said space, during said passing of the liquids, combined electric fields between terminal electrodes from alternating current source; and meansfor periodically cleansing said vessel and adsorption material, and means for removing and gathering therefrom adsorptions, precipitates, aggregations, flocculations and coagulations;

37. An apparatus of the nature described comprising an insulated vessel holding a mass of comminuted solid, suitable electrically-acting adsorption material between electrode terminals; means for maintaining within said vessel an alternating electric field between said electrode terminals from alternating current source regulated as to voltage and frequency and amperage; means for maintaining 'a passage of liquids or fluids through such adsorption material and electric field at regulated pressure and temperature.

38. An apparatus of the nature described comprising a narrow insulated vessel hol'ding a mass of comminuted solid, insoluble, suitable, electrically-acting adsorption material between electrodes; means for maintaining within said vessel an alternating electric field of force between terminal electrodes from alternating current source-regulated as to voltage and frequency and amperage; means for maintaining a passage of liquids or fluids terial'between electrodes; means for maintaining wlthin sald vessel an alternating age; means for maintaining a passage of through such adsorption material and electric field, at regulated pressure and temperature; an electric makeand-break earth connection from-saidliquids .or fluids in synchronism with said alternating current; means for periodically cleansing said vessel and adsorption material, and means. for gathering precipitations, aggregations, flocculations, concentrations and adsorption of substances from within said vessel.

40. The apparatus comprising an insulated vessel holding comminuted solid insoluble dielectric suitable adsorption material, loosely packed between sets of inert plate electrodes, a terminal electrode of one set facing the like terminal electrode of another set, each set of electrodes being connected with the terminals of different c1r-- cuits of a polyphase system of independent symmetrical-alternating currents; means of passing a liquid or fluid rapidly under pres-.

sure through said adsorption material; means of creating, collecting and carrying to said electrodes the said polyphase currents during said passage; means of electrically connecting the liquid to earth while being passed through said electric fields through an exterior interrupter making and breaking earth connection synchronously with said alternating current; means for periodically cleansing said electrodes and adsorption material and vessel, and means for gathering adsorptions and precipitates, aggregations, flocculations, coagulations and the like from said materials and vessel.

41. The apparatus comprising the combination of an insulated vessel; terminal electrodes and intermediate electrodes, arranged in parallel, with narrow space between adjacent electrodes and with comminuted solid adsorption material between all electrodes;

with means of passing a liquid or fluid un-' der pressure continuously through said adsorption material into a dielectric receptacle; the terminal electrodes during said passage being connected with the terminals of a symmetrical alternating current of regulated voltage and frequency and amperage; with means for attemperating said vessel and contents during said passage to between 33 degrees F. and 176 degrees F.; and means for permitting the periodical cleansing of said electrodes and material and vessel, and the gathering of adsorptions, aggregations, precipitates, flocculations and coagulations therefrom.

42. As a new product a stabilized electrically charged liquid, containing therein with enhanced electric charges, colloidal constituents, non-adsorbable by a 'comminuted solid insoluble adsorption material under 44. As a new product a liquid containing emulsoid colloidal constituents but substantially free from adsorbable suspensoid colloidal constituents.

45. As a new product an electrically charged liquid under insulated conditions containing amphoteric colloidal constituents and substantially free from adsorbable colloidal constituents.

46. As a new product, a beer, maltextract, and the like, containing amphoteric colloidal constituents and substantially free from adsorbable colloidalconstituents.

47. As a new product, a beer, malt extract, andthe like, containing amphoteric colloidal constituents carrying electric charges under insulated conditions and substantially free from adsorbable colloidal constituents.

4:8. As'a new product, a liquid freed from suspensoid colloids and comprising emulsoid colloids electrically charged with adsorbed ions, under insulated conditions.

49. As a new product, a beer freed from turbidity-forming colloids and comprising emulsoid colloids electrically charged with adsorbed ions, under insulated conditions.

50. As a new product a stabilized electrically charged substance, containing therein with enhanced electric charged, colloidal constituents, non-adsorbable by a comminuted solid insoluble adsorption material under the influence of an alternating electric field, and being substantially free from colloidal constituents adsorbable by such material under such influence.

51. As a new product a substance containing amphoteric colloidal constituents and substantially free from adsorbable colloidal constituents.

52. As a new product a substance containing emulsoid colloidal constituents but substantially free from adsorbable suspensoid colloidal constituents.

53. As a new product an electrically charged substance under insulated conditions containing amphoteric colloidal constituents and substantially free from adsorbable colloidal constituents.

54. As a new product, a stabilized liquid containing in solution amphoteric colloids carrying charges of electrically-adsorbed lons.

55. As a new product a substance concharges of electrically-adsorbed negative 10 mining therein amphoteric colloids charged ions;

with e ectrically-adsorbed ions. In testimony whereof, I have aflixed my 56. As a new product, a liquid cont'iining signature in the presence of two witnesses.

5 in solution amphoteric colloids carrying charges of electrically adsorbed negative JACOB BLOOM ions. Witnesses: 7

57. As a new product, a beer R. R. Warm,

in solution amphotcric colloids carrying F. E. BARROWS. 

